Manufacturing method of glucose
A manufacturing method, glucose technology, applied in the field of biochemistry, can solve the problems of poor removal of impurities, reduced service life of resin, low product quality and yield, and achieve the effect of improving utilization rate, prolonging service life and good quality
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[0036] Example 1 Obtaining Saccharification Liquid (Prior Art)
[0037] Starch liquefaction: Mix starch and water to prepare a liquid starch emulsion for glucose production. The starch content accounts for 20%-35% of the total mass of the liquid starch emulsion. Then it is sterilized to prepare a starch emulsion, and then to the starch emulsion Add high-temperature amylase to the liquefaction ejector for one high-pressure injection, and then add enzymes for the second time to continue the liquefaction reaction, and hydrolyze into a liquefied starch solution with a glucose value of 14%-25%;
[0038] Saccharification: Cool the liquefied starch solution with a glucose value of 14%-25% prepared in the previous step to 35-45°C, then add compound saccharification enzyme and enzymatically hydrolyze into glucose saccharification solution at this temperature. The saccharification liquid is stored at a height of about 7.5m and a volume of 120m 3 In the saccharification tank, the insoluble pr...
Example Embodiment
[0040] Example 2 One of membrane filtration and impurity removal
[0041] In this embodiment, the microfiltration membrane adopts Asahi Kasei hollow membrane UMP-153, the UMP-153 membrane filament has an inner diameter of 2.6 mm and a pore size of 0.2 um. It can be seen from Table 1 that under the operating conditions of 2.4 bar, the concentration is 5-7 times, the membrane basically does not intercept the product, the flux is maintained between 130LMH-210LMH, and combined image 3 It can be seen that the membrane operation is very stable.
[0042] Table 1 UMP-153 membrane operating data
[0043] Batch
Example Embodiment
[0044] Example 3 Membrane filtration and impurity removal
[0045] In this embodiment, the Asahi Kasei hollow membrane USP-143 is used as the microfiltration membrane. The USP-143 membrane filament has an inner diameter of 1.4 mm and a pore size of 0.1 um. It can be seen from the membrane operating data in Table 2 that the average inlet pressure is about 1.4 bar, the average outlet pressure is about 1.1 bar, and the circulating flow rate is between 1600-2000m3 / h and the temperature is between 42-62℃. About 6 times, there is basically no interception in the glucose production process, the membrane flux is between 150-160LMH; combined with the membrane flux change curve, the membrane flux fluctuates between 160LMH, and the repeatability of 3 batches is good , Indicating that the membrane is running very stable; in addition, from the filtrate test data in Table 5, it can be seen that when the solid content of the feed liquid is high, the light transmittance of the filtrate can basic...
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